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    • 5. 发明专利
    • Regenerating treatment of ion-exchange resin
    • 再生离子交换树脂的处理
    • JPS6174651A
    • 1986-04-16
    • JP19759284
    • 1984-09-20
    • Kansai Paint Co Ltd
    • MITSUYA EIZO
    • B01J49/00B01J49/02
    • PURPOSE: To regenerate efficiently a titled ion-exchange resin by passing a liq. to be treated by using an ion-exchange resin using an OH-type granular anion-exchange resin and an H-type cation-exchange resin as the ion exchange resin.
      CONSTITUTION: A granular anion-exchange resin or a granular cation-exchange resin is treated with a liq. chemical having ion selectivity equivalent to or higher than that of the ion to be removed in a liq. to be treated. Then the liq. to be treated is passed by using an ion-exchange resin using an OH-type granular anion-exchange resin or an H-type granular cation-exchange resin as the exchange resin to regenerate the ion-exchange resin. The granular anion (cation)-exchange resin, wherein an basic group such as a quaternary ammonium group and an amine group or an acidic group such as a sulfonic group, an carboxyl group, etc., is introduced into the constitution as the exchange group, is used in this method.
      COPYRIGHT: (C)1986,JPO&Japio
    • 目的:通过传递液体来有效地再生标题离子交换树脂。 使用OH型粒状阴离子交换树脂和H型阳离子交换树脂作为离子交换树脂使用离子交换树脂进行处理。 构成:颗粒状阴离子交换树脂或粒状阳离子交换树脂用液体处理。 离子选择性等于或高于要在液体中除去的离子的离子选择性的化学物质。 待处理 然后liq。 使用OH型粒状阴离子交换树脂或H型粒状阳离子交换树脂作为交换树脂使用离子交换树脂进行处理,以再生离子交换树脂。 引入作为交换基团的构成中引入季铵基和胺基等碱性基团或磺酸基,羧基等酸性基团的粒状阴离子(阳离子) - 交换树脂 ,用于此方法。
    • 6. 发明专利
    • Reduction of high-electric conductive liquid waste during regeneration of ion-exchange resin and apparatus therefor
    • 在离子交换树脂再生过程中降低高电导率液体废物及其装置
    • JPS5919550A
    • 1984-02-01
    • JP12941482
    • 1982-07-23
    • Ebara CorpToshiba Corp
    • KAWAZU HIDEOHAGIWARA MASAHIROIRIE HIROMITSUOOTANI TAKU
    • B01J49/00B01J49/02C02F1/42
    • PURPOSE: To reduce high-electric conductive liquid waste, by reserving it in liquid waste tanks annexed to columns for regenerating both of cation and anion- exchange resins, and using it for the regeneration of said ion-exchange resin.
      CONSTITUTION: Liquid waste tanks 32, 33 for high-electric conductive liquid waste are annexed to a cation-exchange resin regenerating columns 3 and an anion-exchange resin regenerating column 4. In the regenerators connected to a column 1 for the desalination of condensed water, low-electric conductive liquid waste is reserved in a liquid waste tank 2 directly connected to the desalinator column 1, while high-electric conductive liquid waste is reserved in the liquid waste tanks 32, 33 directly connected to the regenerator columns 3, 4 and used for the regeneration of ion-exchange resins. Thus, an amount of water to be used is saved.
      COPYRIGHT: (C)1984,JPO&Japio
    • 目的:为了减少高导电性废液,通过将其留在用于再生阳离子交换树脂和阴离子交换树脂的柱的液体废液箱中,并将其用于再生所述离子交换树脂。 构成:用于高电导液体废液的液体废液箱32,33附着于阳离子交换树脂再生塔3和阴离子交换树脂再生塔4.在连接到用于冷凝水脱盐的塔1的再生器 在直接连接到脱盐塔1的液体废液箱2中保留低导电性废液,同时在与再生器塔3,4直接连接的液体废液箱32,33中保留高导电性废液, 用于离子交换树脂的再生。 因此,可以节省一定量的水。
    • 8. 发明专利
    • RECOVERY OF VALUABLE IN REGENERATION WASTE WATER OF ION EXCHANGE RESIN
    • JPS562853A
    • 1981-01-13
    • JP7930079
    • 1979-06-23
    • SHINKO PFAUDLER
    • KOGA SHIGETOMAEDA YOSHINORI
    • C02F1/44B01J49/00B01J49/02
    • PURPOSE:To raise the recovery efficiency of valuables and reduce greatly the recovery cost by treating diluted solution of the valuables discharged from ion exchange resin regeneration process by means of an ultrafiltration membrane, etc. CONSTITUTION:A diluted solution of valuables discharged from sweetening-off and sweetening-in processes, among the regenerated waste water of ion exchange resin, is introduced into the tank 2 through the pipe 1, passed through the valve 3, the pump 6, the filter 7, and the pressure pump 8, treated by the ultrafiltration membrane or reverse osmotic membrane separator 4, and then stored in the tank 14 for filtrate and in the tank 9 for concentrate. When the concentrate does not reach a given concentration, it is circulated to the separator 4, and also when a given conentration is reached, it is recovered in the storage tank 9 through the storing pump 20. Also, the filtrate of the tank 14 is sent by the pump 21 to a necessary place to utilize it as regenerated water. Thus, valuables, which have been discarded hitherto, are recovered with consumption of less energy, incidental facilities are made smaller, and the recovering cost is reduced.